Systems and methods for defrosting frozen carbonated beverage systems

ABSTRACT

A system for dispensing a frozen beverage. The system includes a barrel having an inner wall and being configured to retain the frozen beverage therein. A mixing system causes mixing of the frozen beverage within the barrel. A cooling system cools the frozen beverage from radially outwardly of the inner wall. A melting system heats the frozen beverage from radially inwardly of the inner wall. The mixing system causes relatively larger ice crystals to move inwardly from the inner wall, and the melting system reduces a size of the relatively larger ice crystals.

CROSS REFERENCE TO RELATED APPLICATION

This application is a continuation of U.S. Pat. Application No.16/818,082, filed Mar. 13, 2020, which is incorporated herein byreference in its entirety.

FIELD

The present disclosure generally relates to frozen carbonated beveragesystems, and more particularly to systems and methods for defrostingfrozen carbonated beverage systems.

BACKGROUND

The Background and Summary are provided to introduce a foundation andselection of concepts that are further described below in the DetailedDescription. The Background and Summary are not intended to identify keyor essential features of the potentially claimed subject matter, nor arethey intended to be used as an aid in limiting the scope of thepotentially claimed subject matter.

The following U.S. Pat. and Patent Applications are incorporated hereinby reference:

U.S. Pat. No. 5,103,649 discloses improvements in the electronic controlof frozen carbonated beverage machines and defrost heaters therein. Acontrol scheme is shown that provides for accurately determining theviscosity of a semi-frozen beverage as a function of the torque of adrive motor. The viscosity scale has a zero value when the beverage isknown to be completely liquid. Viscosity is maintained within a narrowrange based upon pre-defined three level low, medium and high viscositysets, and wherein compressor short-cycling is eliminated.

U.S. Pat. No. 6,220,047 discloses a dual purpose carbonator/blendingbottle connected to a source of beverage syrup, a source of potablewater and to a source of pressurized carbon dioxide gas. The dualpurpose bottle is retained within an ice bank water bath tank. A pair ofratio valves provide for metering the water and syrup at a desiredratio. A refrigeration system provides for cooling an evaporator locatedin the water tank for forming the ice bank thereon. The carbonatedbeverage then flows from the bottle into a freeze cylinder. A scrapingmechanism within the cylinder provides for scraping frozen beverage fromthe inner surface of the cylinder. A control mechanism provides forcontrolling the refrigeration system and the cooling of bothevaporators.

U.S. Pat. No. 6,830,239 discloses a carbonator tank that includes aliquid inlet, a gas inlet and a liquid outlet. A liquid level sensorincludes a liquid level sensing portion extending along and within theinterior of the carbonator and provides for determining a full andminimal liquid level therein. The liquid then flows into the carbonatorinterior and contacts a deflection plate and is deflected thereby sothat such liquid flow does not disrupt the operation of the levelsensing portion of the level sensor.

U.S. Pat. No. 5,212,954 discloses improvements in electric defrostheaters used in frozen carbonated beverage machines. The frozencarbonated beverage machine includes freeze cylinders used to producethe frozen beverage. One or more tubes are secured in heat exchangerelationship along the exterior of the freeze cylinder. Cartridge typeheating elements are releasably insertable into the tubes to provide fordefrosting of the beverage in the freeze cylinder.

U.S. Pat. Nos. 6,163,095, 8,196,423, 9,062,902, and 9,328,948 furtherrelate to frozen carbonated beverage dispensing systems and variousimprovements thereto.

SUMMARY

This Summary is provided to introduce a selection of concepts that arefurther described below in the Detailed Description. This Summary is notintended to identify key or essential features of the claimed subjectmatter, nor is it intended to be used as an aid in limiting the scope ofthe claimed subject matter.

One embodiment of the present disclosure generally relates to a systemfor dispensing a frozen beverage. The system includes a barrel having aninner wall and being configured to retain the frozen beverage therein. Amixing system causes mixing of the frozen beverage within the barrel. Acooling system cools the frozen beverage from radially outwardly of theinner wall. A melting system heats the frozen beverage from radiallyinwardly of the inner wall. The mixing system causes relatively largerice crystals to move inwardly from the inner wall, and the meltingsystem reduces a size of the relatively larger ice crystals.

Another embodiment generally relates to a method for melting a frozenbeverage within a frozen beverage dispenser, where the frozen beveragebeing contained within inner walls of a barrel. The method includesmixing the frozen beverage within the barrel via a mixing system, wherethe mixing system causes relatively larger ice crystals to move inwardlyfrom the inner wall. The method further includes controlling a coolingsystem to cool the frozen beverage from radially outwardly of the innerwall, and controlling a melting system to alternate between on and offstates, where the melting system heats the frozen beverage from radiallyinwardly of the inner wall only in the on state, and where the meltingsystem reduces a size of the relatively larger ice crystals.

Another embodiment generally relates to a system for dispensing a frozenbeverage. The system includes a barrel having an inner wall extendingbetween a front and a back and being configured to retain the frozenbeverage therein. A mixing system causes mixing of the frozen beveragewithin the barrel, where the mixing system includes a beater barrotatable within the barrel that when rotated causes the frozen beverageto flow from the front of the barrel towards the back along the beaterbar and to flow from the back of the barrel towards the front along theinner wall of the barrel. A cooling system cools the frozen beveragefrom radially outwardly of the inner wall. A melting system heats thefrozen beverage from radially inwardly of the inner wall. A controlsystem controls the melting system to alternate between on and offstates, where the frozen beverage is heated by the melting system onlyin the on state, where the mixing system causes relatively larger icecrystals to move inwardly from the inner wall, and where the meltingsystem reduces a size of the relatively larger ice crystals.

Various other features, objects and advantages of the disclosure will bemade apparent from the following description taken together with thedrawings.

BRIEF DESCRIPTION OF THE DRAWINGS

The drawings illustrate embodiments for carrying out the disclosure. Thesame numbers are used throughout the drawings to reference like featuresand like components. In the drawings:

FIG. 1 is a sectional side view of an exemplary frozen carbonatedbeverage system according to the present disclosure;

FIGS. 2 and 3 depict schematic views of exemplary beverage productionand refrigeration systems for frozen carbonated beverage systemsaccording to the present disclosure, respectively;

FIG. 4 depicts an exemplary process flow for filling a frozen carbonatedbeverage system according to the present disclosure;

FIG. 5 depicts an exemplary process flow for refrigerating a frozencarbonated beverage system according to the present disclosure;

FIG. 6 depicts an exemplary control system for operating a frozencarbonated beverage system according to the present disclosure;

FIG. 7 is a front view of an exemplary barrel for a system according tothe present disclosure;

FIGS. 8A-8C are side views of barrels incorporating embodiments ofheated beater bars according to the present disclosure;

FIG. 9 is a side view of a barrel incorporating a heated grill accordingto the present disclosure; and

FIGS. 10-11B are side views of barrels incorporating remote heatingaccording to the present disclosure.

DETAILED DISCLOSURE

This written description uses examples to disclose embodiments of thepresent disclosure and also to enable any person skilled in the art topractice or make and use the same. The patentable scope of the inventionis defined by the potential claims and may include other examples thatoccur to those skilled in the art. Such other examples are intended tobe within the scope of the claims if they have structural elements thatdo not differ from the literal language of the claims, or if theyinclude equivalent structural elements with insubstantial differencesfrom the literal language of the claims.

The present disclosure generally relates to systems and methods fordispensing frozen carbonated beverages (FCBs), such as may be offered ata food or beverage service provider, a convenience store, or the like.It should be recognized that the presently disclosed systems and methodsalso apply to non-carbonated frozen beverages and food products, forexample. An exemplary system 100 for producing and dispensing FCBsaccording to the present disclosure is shown in FIGS. 1-3 . FIG. 1 showsan exemplary dispensing machine 99, which prepares and stores a beveragewithin a barrel 122 that extends from a back 94 to a front 92. A frontplate 90 is coupled to the front 92 and includes a dispenser valve 166for dispensing the frozen product from the barrel 122. In certainexamples, selections for the beverage to be dispensed are made using auser interface 109. The content within the barrel 122 is cooled (orheated) based on the temperature of fluid flowing through the heattransfer coil 155 substantially encircling the outer perimeter of thebarrel 122 in a conventional manner.

A motor 142 rotates a beater bar 144 and scraper blades 146 attachedthereto, which are also collectively referred to as a mixing system. Insystems 100 known in the art, the beater bar 144 is rotated at a fixedspeed (i.e., 168 RPM). The motor 142 is coupled to the beater bar 144via a motor coupling shaft 148 that passes through a rotary barrel seal150. An expansion tank 134 is also provided between supply lines 107 anda barrel inlet 140 defined within the barrel 122. The power required forthe motor 142 to rotate the beater bar 144 and the scraper blades 146through the mixture contained within the barrel 122 is monitored by acontrol system 600 (FIG. 6 , discussed below) having a processing system610 and memory system 630. This power consumption is then used toestimate the viscosity of product within the barrel 122.

The system 100 includes a beverage production system 101A (FIG. 2 ) anda refrigeration system 101B (FIG. 3 ). In the beverage production system101A of FIG. 2 , pressurized water 102, syrup concentrate 104, and CO2106 (collectively, supply lines 107) are supplied to the system 100.Pressures are monitored by “sold out” pressure switches 108 connected toeach of the supply lines 107. The pressure of the water 102 entering thesystem 100 is controlled by reducing the pressure through a regulator110, then increasing the pressure with a CO2 powered pump 112 to yield aconsistent and known final pressure. The pressure provided by this CO2powered pump 112 is a function of inlet CO2 pressure.

In a similar manner, pressure for the syrup concentrate 104 is suppliedby a CO2 powered pump 114, whereby pressure is again provided as afunction of inlet CO2 pressure as controlled by a regulator. Theresulting pressure of syrup concentrate 104 at the dispensing machine 99(FIG. 1 ) is a function of the pressure provided by the CO2 powered pump114, the distance in elevation between the pump 114 and the dispensingmachine 99, tubing diameters for the supply lines 107, syrup concentrate104 viscosity, the number of splices or joints in the supply lines 107,and other factors.

Continuing with FIG. 2 , the pressure of incoming CO2 106 is controlledby a regulator, which for certain systems 100 is set at 75 psig. Supplypressures may drop for multiple reasons. Since all supply lines 107 mayincorporate the use of CO2 106 as described above (i.e., via CO2 poweredpumps 112 and 114), a reduction in CO2 106 supply pressure can affectall supply lines 107. This can occur when the contents of the CO2 106tank are depleted, when there is an increased draw on the CO2 106 tankfrom other dispensing machines 99 or other devices sharing common CO2106, or an increased draw from a single dispensing machines 99, such asif multiple barrels 122 are filled simultaneously as part of a standardmaintenance activity, for example.

When one of the supply lines 107 is depleted, the pressure of thatsupply line 107 will drop below a “cut off” pressure as read by apressure switch 108. A control system 600 (FIG. 6 ) receives inputs fromthe pressure switch 108 and compares these pressure values to “cut in”and “cut off” values. If the pressure is below the “cut off” pressure,the control system determines that the supply is “sold out.” The controlsystem 600 then signals the need for the supply to be replenished untilthe supply pressure is determined to be above a “cut in” pressure asread by the pressure switch 108. When the control system 600 determinesthat the pressure of the supply line 107 has surpassed the cut inpressure, the control system will no longer indicate that the supplyline 107 is “sold out.” The fill process 168 for this beverageproduction system 101A (FIG. 2 ) is shown in FIG. 4 , which is discussedfurther below.

FIG. 6 depicts an exemplary control system 600 for operating a system100 according to the present disclosure. The control system 600communicates with input devices 602 (which may include pressure switches108, for example), output devices 604 (such as the water valves 124),and/or a cloud 606 based network. In the exemplary control system 600shown, an input/output (I/O) system 620 provides communication betweenthe control system 600 and the input devices 602, output devices 604,and cloud 606, which may each be bidirectional in nature. A processingsystem 610 within the control system 600 is configured to executeinformation received from the I/O system 620 and also from the memorysystem 630. In the example shown, the memory system 630 includes anexecutable program 632 for operating the control system 600 and thesystem 100 more generally, as well as a data 634 module for storing suchparameters as cut in and cut off pressures, as discussed above.

It should be recognized that certain aspects of the present disclosureare described and depicted, including within FIG. 6 , in terms offunctional and/or logical block components and various processing steps.It should be recognized that any such functional and/or block componentsand processing steps may be realized by any number of hardware,software, and/or firmware components configured to perform the specifiedfunctions. For example, certain embodiments employ various integratedcircuit components, such as memory elements, digital signal processingelements, logic elements, look-up tables, or the like, which areconfigured to carry out a variety of functions under the control of oneor more processors or other control devices. The connections betweenfunctional and logical block components are also merely exemplary.Moreover, the present disclosure anticipates communication among andbetween such components being wired, wireless, and through differentpathways

These functions may also include the use of computer programs thatinclude processor-executable instructions, which may be stored on anon-transitory tangible computer readable medium. The computer programsmay also include stored data. Non-limiting examples of thenon-transitory tangible computer readable medium are nonvolatile memory,magnetic storage, and optical storage. As used herein, the term modulemay refer to, be part of, or include an application-specific integratedcircuit (ASIC), an electronic circuit, a combinational logic circuit, afield programmable gate array (FPGA), a processor system (shared,dedicated, or group) that executes code, or other suitable componentsthat provide the described functionality, or a combination of some orall of the above, such as in a system-on-chip. The term module mayinclude memory (shared, dedicated, or group) that stores code executedby the processor. The term code, as used herein, may include software,firmware, and/or microcode, and may refer to programs, routines,functions, classes, and/or objects. The term shared, as used above,means that some or all code from multiple modules may be executed usinga single (shared) processor. In addition, some or all code to beexecuted by multiple different processors as a computer system may bestored by a single (shared) memory. The term group, as used above, meansthat some or all code comprising part of a single module may be executedusing a group of processors. Likewise, some or all code comprising asingle module may be stored using a group of memories as a memorysystem.

Furthermore, certain elements are shown as singular devices for the sakeof clarity, but may be combined or subdivided differently to perform thesame function. For example, the processing system 610 may represent asingle microprocessor, or a group of microprocessors functioning as asystem. This also applies to the input/output (I/O) system 620 andmemory system 630, which may also store information therein in greateror fewer groupings than is shown.

As shown in FIG. 4 , the control system 600 determines the barrel 122pressure in step 202 via inputs received from the pressure switch 108.The control system 600 then compares the barrel 122 pressure to the cutin and cut off values previous described. If the control system 600determines that the pressure is below the cut off value, the controlsystem 600 signals for the barrel 122 to be filled. To fill the barrel122, the water valves 124, syrup valves 126, and CO2 valves 128 areopened to allow water, syrup concentrate, and CO2 to simultaneously flowinto the barrel 122 together. The water 102 and syrup concentrate 104are generally kept at a consistent ratio, set by manually adjustingwater flow controls 130 and syrup concentrate flow controls 131. Forbeverage systems known in the art, water valves 124 and syrup valves 126are controlled in tandem. Depending on the required amount of CO2, theCO2 valve 128 may open fully when the water valves 124 and syrup valves126 are opened, or may open intermittently, such as via a specified dutycycle.

The water 102, syrup concentrate 104, and CO2 106 pass through theliquid side 132 of an expansion tank 134. The expansion tank 134 ispressurized on the gas side 136 of an internal diaphragm 138, whichallows for expansion of the liquid contents of the machine duringfreezing without damaging the rest of the rigid components within themachine. Liquid product then enters the barrel 122 through a barrelinlet 140 (FIG. 1 ).

Continuing with reference to FIGS. 2 and 4 , the state of the fillprocess 168 continues in step 206 (whether filling or not filling) aslong as the barrel 122 pressure is between the cut in and cut offvalues. However, if the pressure in the barrel 122 is determined to beat or above the cut in value in step 208, the water valves 124, syrupvalves 126, and CO2 valves 128 are all closed to stop the fill process168 in step 210.

A similar control process occurs with respect to the refrigerationsystem 101B (FIG. 3 ), which is shown in the refrigeration process 180of FIG. 5 . In particular, the viscosity of contents in the barrel 122is used to determine whether the beverage requires more, less, or thesame refrigeration at any given time. The viscosity is determined basedon the power required by the motor 142, which is read in step 250. Thecontrol system 600 (FIG. 6 ) then determines whether the viscosity fallsbelow a stall value in step 252, based on comparison to a table storedwithin the data 634 of the memory system 630. If the viscosity is foundto be greater than the stall value in step 252, the motor 142 is stoppedin step 264 and a defrost process is started to melt the excessive icecausing the excessive viscosity within the barrel 122, ending at step262.

If alternatively the viscosity is determined in step 252 to be below thestall value, the process continues with determining an action in step254 based on whether the viscosity is below, above, or between cut inand cut out values (also stored in the data 634 of the memory system630). If it is determined in step 254 that the viscosity is below thecut in value (meaning low), refrigeration is engaged in step 256,freezing additional content within the barrel 122 to increase theviscosity therein. If alternatively the viscosity is above a stored cutout value, refrigeration is discontinued in step 260 to prevent afurther increase in viscosity. Finally, if the viscosity is determinedin step 256 to be between the cut in and cut out values, therefrigeration process 180 continues the previous refrigeration step 258and the process is repeated.

As shown in FIG. 3 , the refrigeration system 101B includes a compressor154 and condenser 156 for the system 100, as well as liquid linesolenoid valves 158, hot gas solenoid valves 160, and expansion valves162 for each barrel evaporator 164. In this manner, the system 100 maysupply refrigeration or heat to each barrel 122 independently. In freezemode, the refrigeration system 101B draws heat out of the barrel 122through the evaporator until the viscosity of the product meets aspecified cut out value, as discussed above. As beverages are dispensed,product is pushed out of the dispense valve 166 (FIG. 1 ) by pressurewithin the barrel 122. As the barrel 122 pressure drops below aspecified minimum fill pressure, the fill process 168 (FIG. 4 ) resumesuntil barrel 122 pressure reaches a specified maximum fill pressure.During the fill process 168, liquid product enters the barrel 122 atambient temperature through a barrel inlet 140 (FIG. 1 ). Heat thereforeenters the barrel 122 through conduction and friction. As previouslystated, the viscosity of the product decreases until it meets aspecified cut in value, caused by this heat, until refrigeration beginsagain.

As shown in FIG. 7 , during the refrigeration process 180 previouslydiscussed, ice crystals 170 form on the inside wall 172 of the barrel122 (FIG. 1 ), which are scraped off the inside wall 172 by the scraperblades 146 coupled via supports 145 to the beater bar 144. The presentinventors have identified through experimentation and research that overtime and through multiple refrigeration cycles, the ice crystals 170 inthe barrel 122 grow in size and stick together to form larger icecrystals 174 and large ice formations 176, degrading the smooth textureof the drink produced by the system 100. As the barrel 122 contentsrotate, higher density components are driven towards the perimeter ofthe barrel 122 via centripetal force, likewise forcing lower densitycomponents (such as the larger ice crystals 174 and large ice formations176) towards the center of the barrel 122. This in turn results inlarger formations of ice 176 surrounding the beater bar 144, leading toundesirable and/or inconsistent product.

After a specified time, the barrel 122 enters a defrost cycle where heatis added to the barrel 122 through the heat transfer coil 155 via thebarrel evaporator 164 (FIG. 3 ) for a set duration, or until thetemperature of the evaporator outlet 178 reaches a specifiedtemperature. In certain examples, the intention of this defrost cycle isto fully melt all product in the barrel 122. From there, therefrigeration process 180 begins again until the viscosity of theproduct meets a specified cut out value, as discussed with respect tothe process flow of FIG. 5 .

The present inventors have identified that FCB systems presently knownin the art are prone to several types of problems. For example, aproblem arises when the pressure in a supply line 107 (such as water102, syrup concentrate 104, or CO2 106) falls below a specified value.In this case, the dispensing machine 99 in certain systems 100 willdisable the fill process 168 to prevent an improper mix of ingredientsfrom entering the barrel 122. Likewise, problems arise when theviscosity of the barrel 122 exceeds a specified safety value intended toprevent damage to the system 100. In this case, the motor 142 istypically disabled and a defrost cycle begins to melt the excess icethat is presumed to be building up within the barrel 122.

The present disclosure further relates to improved systems and methodsfor controlling the size of ice crystals in a frozen beverage products.In particular, the freezing and defrost cycles for FCB systems presentlyknown in the art require frequent down time, and consequently a loss ofbeverage sales for system owners. As discussed above, systems presentlyknown in the art conduct defrost cycles at a fixed interval, such as acertain period of time (for example, every 3 hours).

The current process for defrosting in systems known in the art is tocontrol the size of ice crystals 170 by fully melting the contents ofthe barrel 122 to an entirely liquid, baseline state, then refreezingit. The inventors have identified that this has multiple disadvantages.First, the resultant product within the barrel 122 after the defrostcycle is not at the desired consistency, but must be refrozen asdiscussed above. Moreover, both the defrost cycle and refreezing cycleare energy-intensive processes. Additionally, acceptable beveragescannot be dispensed during at least the defrost cycle, resulting in lostsales from downtime. To minimize the duration of the defrost cycle, thefull capacity of the compressor 154 (FIG. 1 ) is dedicated to defrostinga single barrel 122, whereas multiple barrels 122 may be present withinthe system 100. Any diversional of this capacity to defrost multiplebarrels 122 in tandem, or to continue refrigeration of other barrels 122during this process, extends the duration of the defrost cycle andthereby increases the amount of time that a given barrel 122 is notavailable to dispense beverages.

Furthermore, in configurations that incorporate a remote condenserserving multiple FCB systems and/or other products, it is traditional tomount the compressor and condenser in a remote location to minimize theamount of heat and noise thereby produced. However, systems presentlyknown in the art use hot gas for the defrost cycle, which preferencesthe compressor being inside the system. This reduces the opportunitiesfor smaller, quieter equipment. This also creates the risk that, inerror conditions, the contents of the barrel may be heated to dangeroustemperatures, requiring further complication for additional safetymeasures.

The inventors have identified that with systems presently known in theart, the size of the ice formation is inconsistent within the barrel.The inventors further identified that this inconsistency is causedand/or exacerbated by treating and monitoring the contents within thebarrel as if this content were uniform. Through experimentation andresearch, the inventors have developed the presently disclosed systemsand methods for improving consistency within the barrel 122. In general,these systems and methods relate to melting the largest pieces of iceformed within the barrel 122 of the system 100, providing uniformity andthe desired consistency for product being dispensed.

With reference to FIG. 7 , the inventors have identified that over time,ice crystals 170 (FIG. 7 ) coalesce and become larger ice crystals 174and eventually larger formations of ice 176. This growth is influencedby several factors, including the composition of the content within thebarrel 122 (such as the percent sugar), the temperature inside thebarrel 122, the frequency and/or volume of drinks being dispensed fromthe barrel 122 and subsequently replaced by unfrozen product, thetemperature of the unfrozen product entering the barrel 122, and/or thespeed of rotation of the barrel 122 being agitated by an agitator orbeater bar 144, for example. As discussed above, rotation of the barrel122 over time causes higher density components (e.g., syrup concentrate104) to migrate towards the inside wall 172 of the barrel 122, and lowerdensity components (i.e., ice crystals 170) towards the center of thebarrel 122, surrounding the beater bar 144. This separation may befurther impacted by the surface finish, material, or the geometry of thebeater bar 144, inside wall 172, and/or other characteristics of thebarrel 122 generally.

FIGS. 8A-11B depict various embodiments of systems 100 according to thepresent disclosure for improving the defrost cycle and, likewise, theconsistency of the content within the barrel 122. A first family ofsolutions generally relates to heating of the beater bar 144, since thelower density ice crystals 170 migrate towards the beater bar 144 aspreviously described. In particular, the present inventors haveidentified that the ice crystals 170 surrounding the beater bar 144 canbe melted by heating the beater bar 144. As the ice crystals 170 melt,their corresponding densities increase. This allows the now-meltedcontent to migrate away from the beater bar 144 upon further rotation,subsequently being replaced by lower density ice crystals 170 for theprocess to repeat. The defrost cycle is controlled by the control system600 (FIG. 6 ) in the manner previously described, which may operatebased on time intervals, temperatures at one or more locations withinthe barrel 122, viscosity readings at one or more locations within thebarrel 122, or combinations thereof.

FIGS. 8A-8C depict various embodiments for heating the beater bar 144 toaccomplish this targeted melting process. In the embodiment of FIG. 8A,the beater bar 144 is heated via inductive power provided to heatingelements therein. As shown, a first fixed coil 302 is coupled to anelectrical source (not shown) within the system 100, whereby the fixedcoil 302 is located coaxially around a core 304. The core 304 (which mayalso be the motor coupling shaft 148 of FIG. 1 ) includes a secondrotating coil 306 that is coupled to heating elements 308 within thebeater bar 144. In this manner, when alternating current (AC) issupplied to the fixed coil 302, it induces AC current in the rotatingcoil 306 to thereby power the heating elements 308. These heatingelements 308 may be embedded in a cast or molded beater bar 144, orapplied over the surface of an otherwise known beater bar 144, forexample. This in turn melts the ice crystals 170 surrounding the beaterbar 144 as previously discussed. In this manner, the embodiment of FIG.8A heats the beater bar 144 by functioning as a transformer.

FIG. 8B shows an alternate embodiment for heating of the beater bar 144.In this embodiment, the beater bar 144 itself is heated throughinduction. A first fixed coil 302 is coupled to an electrical source(not shown) in the system 100 and is again located coaxially around thebeater bar 144 in the same manner discussed above. However, in thisembodiment, the beater bar 144 is or contains metal such that it isheated when the fixed coil 302 is energized. In this manner, theembodiment of FIG. 8B heats the beater bar 144 by functioning as aninduction heater.

FIG. 8C discloses a third embodiment for heating the beater bar 144according to the present disclosure. In the example shown, the heatingelement 310 is provided as a fixed core that is received within thecenter of the beater bar 144. In certain examples, the heating element310 is fixed relative to the system 100 and is heated by a fixed coil302 in the manner previously described. The heat from the heatingelement 310 then radiates outwardly to the beater bar 144 to accomplishthe localized melting of ice crystals 170 desired.

FIG. 9 discloses an alternate type of embodiment that incorporates aheated grill 314 for melting ice crystals 170, and specifically largerice crystals 174 or larger formations of ice 176 (FIG. 7 ). In theexample shown, a flow pattern for the product is produced between thefront 92 and the back 94 of the barrel 122 through the addition ofblades 312 or other elements associated with beater bar 144 and/orinside wall 172. In the example of FIG. 9 , this flow provides formovement from the front 92 to the back 94 closer to the beater bar 144,and from the back 94 to the front 92 closer to the inside wall 172 ofthe barrel 122.

The grill 314 in the present embodiment is a coil of individual wires315 coupled via connections 317 to a power source (not shown) to beheated, for example as a resistance based heater. The grill 314 incertain embodiments is similar to that of a conventional electric stoveheating element, for example. The individual wires 315 are coiled toform a gap G therebetween (which may vary or be the same across thegrill 314). The grill has an inner diameter ID and an outer diameter OD,which in the example of FIG. 9 is smaller than a barrel diameter BDwithin the inner walls 172 of the barrel 122. As the product flowsthrough the barrel 122, the grill 314 is positioned within the barrel122 to capture larger ice crystals 174 above a specified size,consequently melting them. Specifically, the size of ice captured isselected based on the size of the gap G between individual wires 315. Incertain examples, the grill 314 is positioned near the rear of thebarrel 122. This grill 314 may be a heating element itself, or mayretain the larger ice crystals 174 in proximity to a separate heatingelement (not shown). Melted product 316 then passes along the insidewall 172 of the barrel 122, which subsequently refreezes as it proceedstowards the front 92 of the barrel 122. By the time the product reachesthe front 92 of the barrel 122, it is optimally once again frozenproduct 318 ready for dispensing.

FIG. 10-11B depict another type of embodiment for melting larger icecrystals 174, generally relating to a process of remote heating.Specifically, product may be forced to flow out of the barrel 122, whereit is melted and reintroduced to freeze again within the barrel 122. Aswill be discussed further below, this may be accomplished as acontinuous process, or as a cyclical or periodic process. The frequencyand/or intensity of the process may be governed by various parameters,including the present operational state and/or settings of the system100 (i.e., freezing, defrosting, etc.), the volume of beverage dispensedover a period of time, and the like.

FIG. 10 shows a first type of remote heating that includes arecirculating melt circuit 301. Product is driven out of the barrel 122via a barrel outlet 141 and into the circuit 301, where it is melted andreturned back to the barrel 122 via a barrel inlet 140. This product maybe driven through the circuit 301 by the flow 320 caused by the beaterbar 144, and/or by a separate pump 322, for example. Once the productexits the barrel 122, it is either partially melted (such as with agrill 314 or other heat device, and/or a filter designed to capture icecrystals 170 of a certain size), or be fully melted. Heat may beprovided within the circuit 201 using the heat generated by the system100 itself (such as from the motor 142, condenser 156, or othercomponents within the system 100), or with separate heating elements.For example, a heat transfer region 303 of the circuit 301 may bepositioned to transfer heat from the motor 142. In certain examples,heat may also or alternatively be provided by running the circuit 301such that a heat exchange occurs with warmer, unfrozen product. Thisprovides the added benefit of also pre-cooling the liquid product usedto fill the barrel 122 as beverages are dispensed.

In addition to selectively melting content within the barrel 122, theinventors have further identified that by holding some portion ofchilled product outside of the barrel 122, additional capacity isrealized for the overall system 100.

FIGS. 11A and 11B depict another embodiment providing remote heating fordefrosting content within the barrel 122 according to the presentdisclosure. In the example shown, a cyclical melt is provided by drawinga volume of product out of the barrel 122 via the barrel outlet 141,melting this volume, and then reintroducing the product to the barrel122 to once again be refrozen (which may again be via the barreloutlet). In the example shown, a piston 324 is used to draw the productout of the barrel 122, though other methods may be employed. In oneembodiment, one side of a heat cylinder 334 is fluidly coupled to thebarrel 122, with the other side of the cylinder 334 being coupled via athree-way valve 326 to both a source of pressurized gas on the gas side328 and to a vent 330 to atmosphere. A piston 324 is moveable within theheat cylinder 334 via pressure differential in a manner known in theart, for example.

In the embodiment shown, the gas side 328 of the cylinder 334 is ventedto atmosphere to allow the pressure of the barrel 122 to drive thefrozen product 332 to the product side of the cylinder 338 (FIG. 11A).The product is then heated via a separate heating element as would becommercially available, and/or via heat transfer with the motor 142and/or other elements, causing at least a partial melt thereof. Afterthe product has been at least partially melted, the gas side 328 of thecylinder 334 is repressurized to the operating pressure of the barrel122 such that the product is returned as liquid cylinder contents 340back into the barrel 122 (FIG. 11B). In alternate embodiments, aplurality of cylinders 334 may be utilized to cycle the product throughthe melting cycle process without any dispensing or filling of thebarrel 122.

The present inventors have further identified that the embodiment ofFIGS. 11A-11B offers the additional benefit of incorporating a variablevolume storage reservoir, which has the potential for concurrentlyserving the purposes of the expansion tank 134 (FIG. 1 ) previouslydiscussed. In this manner, the expansion tank 134 could be eliminatedfrom the system 100, thereby reducing further expenses for implementingthe presently disclosed systems and methods.

In the above description, certain terms have been used for brevity,clarity, and understanding. No unnecessary limitations are to beinferred therefrom beyond the requirement of the prior art because suchterms are used for descriptive purposes and are intended to be broadlyconstrued. The different assemblies described herein may be used aloneor in combination with other devices. It is to be expected that variousequivalents, alternatives and modifications are possible within thescope of any appended claims.

What is claimed is:
 1. A system for dispensing a frozen beverage, thesystem comprising: a barrel configured to retain the frozen beveragetherein; a cooling system that cools the frozen beverage; and a meltingsystem that heats a portion of the frozen beverage that has exited thebarrel before the portion of the frozen beverage reenters the barrel. 2.The system according to claim 1, wherein the barrel extends between afront and a back with sides therebetween, wherein the frozen beverage isdispensable from the front of the barrel, and wherein the frozenbeverage exits the barrel on a same one of the front, the back, and thesides that the frozen beverage reenters the barrel after being heated bythe melting system.
 3. The system according to claim 1, wherein thebarrel extends between a front and a back, wherein the frozen beverageis dispensable from the front of the barrel, and wherein the frozenbeverage reenters the barrel horizontally closer to the back than to thefront.
 4. The system according to claim 4, wherein the frozen beverageexits the barrel horizontally closer to the back than to the front. 5.The system according to claim 1, wherein the frozen beverage reentersthe barrel vertically higher than where the frozen beverage exits thebarrel to be heated by the melting system.
 6. The system according toclaim 1, wherein the barrel extends between a front and a back, whereinthe frozen beverage is dispensable from the front of the barrel, andwherein the frozen beverage is heated by the melting system horizontallybehind the back of the barrel so as to be heated farther from the frontof the barrel than from the back of the barrel.
 7. The system accordingto claim 1, further comprising a motor for mixing the frozen beverage,wherein the motor generates heat, and wherein the portion of the frozenbeverage is heated via the heat from the motor.
 8. The system accordingto claim 1, further comprising a pump that causes the frozen beverage toflow between exiting the barrel and reentering the barrel.
 9. A systemfor dispensing a frozen beverage, the system comprising: a barrelconfigured to retain the frozen beverage therein; a cooling system thatcools the frozen beverage; and a mixing system that mixes the frozenbeverage within the barrel, wherein the mixing system is heated so as toheat the frozen beverage while mixing.
 10. The system according to claim9, wherein the mixing system includes a beater bar that rotates withinthe barrel to mix the frozen beverage.
 11. The system according to claim10, wherein the beater bar is heated via induction to thereby heat thefrozen beverage while mixing.
 12. The system according to claim 11,wherein the beater bar is rotated by a motor having a shaft, wherein theinduction is provided by powering a coil, and wherein the coil coaxiallysurrounds the shaft of the motor.
 13. The system according to claim 11,wherein the beater bar comprises a heating element and a first coil,further comprising a second coil configured such that powering thesecond coil induces a current in the first coil to thereby power theheating element of the beater bar.
 14. The system according to claim 13,wherein the first coil is electrically coupled to the heating element.15. The system according to claim 13, wherein the first coil is insidethe barrel and the second coil is outside the barrel.
 16. The systemaccording to claim 11, wherein the beater bar comprises metal, furthercomprising a coil that encircles a portion of the beater bar and isconfigured such that powering the coil heats the beater bar directly viainduction.
 17. The system according to claim 16, wherein the coil isoutside the barrel and is coaxially aligned with the beater bar.
 18. Thesystem according to claim 11, wherein the beater bar comprises a heatingelement, further comprising a coil that encircles a portion of thebeater bar and is configured such that applying electricity to the coilpowers the heating element.
 19. The system according to claim 18,wherein the heating element extends within a core inside the beater bar.20. The system according to claim 18, wherein the coil is outside thebarrel and is coaxially aligned with the heating element within thebeater bar.